EP3285324B1 - Électrolyte polymère à structure multicouche, et batterie tout solide le comprenant - Google Patents

Électrolyte polymère à structure multicouche, et batterie tout solide le comprenant Download PDF

Info

Publication number
EP3285324B1
EP3285324B1 EP16860299.3A EP16860299A EP3285324B1 EP 3285324 B1 EP3285324 B1 EP 3285324B1 EP 16860299 A EP16860299 A EP 16860299A EP 3285324 B1 EP3285324 B1 EP 3285324B1
Authority
EP
European Patent Office
Prior art keywords
polymer electrolyte
lithium
solid battery
solid
polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP16860299.3A
Other languages
German (de)
English (en)
Other versions
EP3285324A1 (fr
EP3285324A4 (fr
Inventor
Dong Wook Ko
Doo Kyung Yang
Eun Kyung Park
Jong Hyun Chae
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
LG Chem Ltd
Original Assignee
LG Chem Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by LG Chem Ltd filed Critical LG Chem Ltd
Priority claimed from PCT/KR2016/012283 external-priority patent/WO2017074116A1/fr
Publication of EP3285324A1 publication Critical patent/EP3285324A1/fr
Publication of EP3285324A4 publication Critical patent/EP3285324A4/fr
Application granted granted Critical
Publication of EP3285324B1 publication Critical patent/EP3285324B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0565Polymeric materials, e.g. gel-type or solid-type
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0568Liquid materials characterised by the solutes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0585Construction or manufacture of accumulators having only flat construction elements, i.e. flat positive electrodes, flat negative electrodes and flat separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/449Separators, membranes or diaphragms characterised by the material having a layered structure
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0082Organic polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0088Composites
    • H01M2300/0094Composites in the form of layered products, e.g. coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/497Ionic conductivity
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a polymer electrolyte with a multi-layer structure for an all-solid-state battery and, more particularly, to a polymer electrolyte having a multi-layer structure, which comprises a first polymer electrolyte layer and a second polymer electrolyte layer, wherein the EO : Li molar ratio of a poly(ethylene oxide)(PEO)-based polymer and a lithium salt is different between the first and second polymer electrolyte layers.
  • secondary batteries particularly lithium-based secondary batteries have higher capacity density than other secondary batteries and can operate at higher voltages, and thus are used for information-related devices or communication devices as secondary batteries for miniaturization and light weight. Recently, the development of high power and high capacity lithium-based secondary batteries for electric vehicles or hybrid vehicles is underway.
  • a typical lithium-based secondary battery consists of a positive electrode (cathode), a negative electrode (anode) and an electrolyte containing lithium salt interposed therebetween, and this electrolyte may be a non-aqueous liquid electrolyte or a solid electrolyte.
  • this electrolyte may be a non-aqueous liquid electrolyte or a solid electrolyte.
  • the lithium-based secondary battery uses a flammable organic solvent in the liquid electrolyte, in order to prevent ignition or rupture that may occur due to over current caused by short, it may be necessary to install a safety device. In addition, in order to prevent such a phenomenon, there are cases where the selection of the battery material or the design of the battery structure is restricted.
  • the all-solid battery since the all-solid battery does not contain a flammable organic solvent, the all-solid battery has the advantage of simplifying the safety device and thus is recognized as a superior battery in terms of manufacturing cost or productivity.
  • the all-solid battery since it is easy to laminate, in series, a pair of electrode layers including a positive electrode (cathode) layer and a negative electrode (anode) layer, and a junction structure including a solid electrolyte layer lying between these electrode layers, the all-solid battery is expected to be a technology capable of producing a high-capacity and high-output battery with stability.
  • LiNbO3 -coated LiCoO2 as cathode material for all solid-state lithium secondary batteries LiNbO 3 (lithium niobate) is described as a material to be coated on the surface of LiCoO 2 (positive electrode active material).
  • This technique aims to obtain a high-power battery in such a manner that the surface of the LiCoO 2 is coated with LiNbO 3 to suppress the reaction between LiCoO 2 and the solid electrolyte material, thereby reducing the interfacial resistance between LiCoO 2 and the solid electrolyte material.
  • Japanese Laid-Open Patent Publication No. 2004-206942 discloses an all-solid battery wherein a second solid electrolyte layer, which does not chemically react with the first solid electrolyte and has lower ion conductivity than the first solid electrolyte layer (sulfide based solid electrolyte material), is formed between the first solid electrolyte layer and a negative electrode made of metal lithium. This application attempts to inhibit the reaction between the first solid electrolyte layer and the metal lithium through formation of the second solid electrolyte layer with low ion conductivity.
  • the all-solid battery to which a solid polymer electrolyte was applied is difficult to exhibit sufficient output or capacity even at room temperature, as well as at 60 ⁇ or 80 ⁇ . For this reason, first, the low ionic conductivity of the polymer electrolyte and second, the interfacial resistance between lithium and the polymer electrolyte can be mentioned. Many efforts have been made to solve the ion conductivity of the polymer electrolyte in the interim, but there was no remarkable improvement in ion conductivity and it has been pointed out as a limitation of the solid polymer electrolyte.
  • the present inventors in view of this, have come to complete the present invention by applying a polymer electrolyte using a high concentration of lithium salt to the all-solid battery to lower the interfacial resistance between lithium and the solid polymer electrolyte.
  • the purpose of the present invention is to provide a polymer electrolyte for the all-solid battery, which significantly reduces the interfacial resistance between lithium and the polymer electrolyte.
  • the present invention provides a polymer electrolyte with multi-layer structure for an all-solid battery, which comprises a first polymer electrolyte layer having a molar ratio of EO : Li of poly (ethylene oxide) (PEO) -based polymer and lithium salt of 1 : 1 to 7 : 1; and a second polymer electrolyte layer having a molar ratio of EO : Li of poly (ethylene oxide) - based polymer and lithium salt of 8 : 1 to 30 : 1.
  • the thickness of the first polymer electrolyte layer may be 1 to 5 ⁇ m.
  • the thickness of the second polymer electrolyte layer may be 5 to 50 ⁇ m.
  • the weight average molecular weight (Mw) of the poly (ethylene oxide) -based polymer may be 1,000,000 to 8,000,000.
  • the lithium salt may include one selected from the group consisting of LiCl, LiBr, LiI, LiClO 4 , LiBF 4 , LiB 10 Cl 10 , LiPF 6 , LiCF 3 SO 3 , LiCF 3 CO 2 , LiAsF 6 , LiSbF 6 , LiAlCl 4 , CH 3 SO 3 Li, CF 3 SO 3 Li, LiSCN, LiC(CF 3 SO 2 ) 3 , (CF 3 SO 2 ) 2 NLi, (FSO 2 ) 2 NLi, chloroborane lithium, lithium lower aliphatic carboxylate, lithium tetraphenylborate, lithium imide, and combinations thereof.
  • the second polymer electrolyte layer may be crosslinked by a crosslinking monomer to form semi-Interpenetrating Polymer Networks (semi-IPN).
  • the crosslinking monomer may contain -(CH 2 -CH 2 -O)-repeating units.
  • the crosslinking monomer may contain 2 to 8 alkylenic unsaturated bonds at the terminals.
  • the crosslinking monomer may be contained in an amount of 5 to 50 wt.% relative to the poly (ethylene oxide)-based polymer and lithium salt.
  • the present invention also provides an all-solid battery comprising a positive electrode, a negative electrode and a solid polymer electrolyte interposed therebetween, characterized in that the solid polymer electrolyte is the polymer electrolyte with the multi-layer structure for the all-solid battery.
  • the first polymer electrolyte layer may be disposed facing the negative electrode.
  • the solid polymer electrolyte of the present invention When the solid polymer electrolyte of the present invention is applied to the all-solid battery, the interfacial resistance with lithium and the discharge overvoltage are significantly reduced, thereby resulting in sufficient discharge capacity and improving output characteristics and energy density.
  • the polymer electrolyte of the present invention applicable to the all-solid battery as the lithium secondary battery is a polymer electrolyte with a multilayer structure, comprising a first polymer electrolyte layer and a second polymer electrolyte layer which include poly (ethylene oxide) (PEO)-based polymer and lithium salt and are different in EO : Li molar ratios of the poly (ethylene oxide)-based polymer and lithium salt.
  • PEO poly (ethylene oxide)
  • the first polymer electrolyte layer is applied to lower the interfacial resistance and is prepared by selecting the molar ratio of EO : Li of poly (ethylene oxide) -based polymer and lithium salt within the range of 1 : 1 to 7 : 1.
  • EO Li of poly (ethylene oxide) -based polymer
  • lithium salt when lithium salt is doped at a high ratio and accordingly thinned to a thickness of 1 to 5 ⁇ m, the ionic conductivity is somewhat lowered, but the interfacial resistance can be significantly lowered.
  • the second polymer electrolyte layer is applied to prevent the phenomenon due to the generation of dendrite by increasing the mechanical strength, and is prepared by selecting the molar ratio of EO : Li of poly (ethylene oxide)-based polymer and lithium salt within the range of 8 : 1 to 30 : 1. At this time, the thickness of the second polymer electrolyte layer may be 5 to 50 ⁇ m.
  • the second polymer electrolyte layer may be crosslinked by a crosslinking monomer to form a semi-Interpenetrating Polymer Networks (hereinafter, referred to as semi-IPN) structure.
  • This semi-IPN structure can increase the strength of the solid polymer electrolyte and, as the strength is high, the generation of lithium dendrite on the surface of the electrode can be physically suppressed.
  • Mw weight average molecular weight
  • the poly (ethylene oxide)-based polymer is applied in a relatively high molecular weight in the range of 1,000,000 to 8,000,000, a more compact semi-IPN structure can be formed.
  • a crosslinking monomer a polyfunctional monomer having two or more functional groups can be used, and such monomer preferably contains -(CH 2 -CH 2 -O)- repeating units and polymerizable alkylenic unsaturated bonds in the range of 2 to 8 at both terminals.
  • the alkylenic unsaturated bond is a hydrocarbon group containing at least one carbon-carbon double bond or triple bond, and includes, but not limited to, ethenyl group, 1-propenyl group, 2-propenyl group, 2-methyl-1-propenyl group, 1-butenyl group, 2-butenyl group, ethynyl group, 1-propynyl group, 1-butynyl group, 2-butynyl group and the like.
  • These alkylenic unsaturated bonds act as crosslinking points to crosslink the poly (ethylene oxide) -based polymer through a polymerization process, thereby forming a semi-IPN structure.
  • the crosslinking monomer may be selected from the group consisting of polyethylene glycol diacrylate (PEGDA), polyethylene glycol dimethacrylate (PEGDMA), poly (propylene glycol) diacrylate : PPGDA), poly (propylene glycol) dimethacrylate (PPGDMA), and combinations thereof, and preferably, polyethylene glycol diacrylate (PEGDA) can be used.
  • PEGDA polyethylene glycol diacrylate
  • PEGDMA polyethylene glycol dimethacrylate
  • PPGDA poly (propylene glycol) diacrylate
  • PPGDMA poly (propylene glycol) dimethacrylate
  • PEGDA polyethylene glycol diacrylate
  • the crosslinking monomer is preferably contained in an amount of 5 to 50 wt.% relative to the weight of the poly (ethylene oxide)-based polymer to form a semi-IPN structure meeting the object of the present invention.
  • crosslinking the crosslinking monomer between the poly (ethylene oxide)-based polymers there is no particular limitation on the method of crosslinking the crosslinking monomer between the poly (ethylene oxide)-based polymers, but preferably the crosslinking monomer can be crosslinked while maintaining a proper temperature condition after adding a thermal initiator. At this time, it is possible to apply benzoyl peroxide (BPO) or azobisisobutyronitrile (AIBN) as a thermal initiator.
  • BPO benzoyl peroxide
  • AIBN azobisisobutyronitrile
  • the lithium salt which is commonly applied to the first polymer electrolyte layer and the second polymer electrolyte layer according to the present invention, can be dissociated into lithium ions and can permeate into the first polymer electrolyte layer and the second polymer electrolyte layer to move freely.
  • the basic operation of the lithium battery is possible by the source of lithium ions, and these lithium salts can be used as long as they are commonly used in lithium batteries, and preferably, the lithium salt includes LiCl, LiBr, LiI, LiClO 4 , LiBF 4 , LiB 10 Cl 10 , LiPF 6 , LiCF 3 SO 3 , LiCF 3 CO 2 , LiAsF 6 , LiSbF 6 , LiAlCl 4 , CH 3 SO 3 Li, CF 3 SO 3 Li, LiSCN, LiC(CF 3 SO 2 ) 3 , (CF 3 SO 2 ) 2 NLi, (FSO 2 ) 2 NLi, chloroborane lithium, lithium lower aliphatic carboxylate, lithium tetraphenylborate, lithium imide, and combinations thereof, and more preferably, lithium bis(fluorosulfonyl) imide (LiFSI) represented by (FSO 2 ) 2 NLi can be used as the lithium salt.
  • LiFSI lithium
  • the method of preparing the first polymer electrolyte layer or the second polymer electrolyte layer of the present invention is not limited in the present invention, and the mixing and molding process by the wet or dry method as known in the art may be used. Also, the thickness of the solid polymer electrolyte of the present invention can be selected within the range of 1 to 50 ⁇ m.
  • An all-solid battery comprising the solid polymer electrolyte of the present invention interposed between the positive electrode and the negative electrode is described, wherein the first polymer electrolyte layer faces the negative electrode and the interfacial resistance is significantly reduced.
  • each electrode active material may be any active material applied to conventional electrodes, and is not particularly limited in the present invention.
  • the positive electrode or negative electrode active material used in the present invention varies depending on the type of conducting ions of the all-solid battery intended. For example, if the all-solid battery according to the present invention is an all-solid lithium secondary battery, the positive electrode or negative electrode active material occludes or releases lithium ions. In addition, the positive electrode or negative electrode active material used in the present invention can typically react with the solid electrolyte material described above to form a high-resistance portion.
  • the positive electrode active material can be varied depending on the usage of the lithium secondary battery, and a known material is used for the specific composition.
  • such positive electrode active material may be any one of lithium transition metal oxides selected from the group consisting of lithium-phosphate-iron compound, lithium cobalt-based oxide, lithium manganese-based oxide, lithium copper oxide, lithium nickel-based oxide, lithium manganese composite oxide, and lithium-nickel-manganese-cobalt-based oxide.
  • the lithium metal phosphorous oxides represented by Li 1+a M(PO 4 - b )X b the lithium metal phosphorous oxides wherein M is at least one selected from the metals of Groups 2 to 12 and X is at least one selected from F, S and N, -0.5 ⁇ a ⁇ +0.5, and 0 ⁇ b ⁇ 0.1 are preferable.
  • the negative electrode active material can be one selected from the group consisting of lithium metal, lithium alloy, lithium metal composite oxide, lithium containing titanium composite oxide (LTO), and combinations thereof.
  • the lithium alloy may be an alloy of lithium and at least one metal selected from Na, K, Rb, Cs, Fr, Be, Mg, Ca, Sr, Ba, Ra, Al and Sn.
  • the lithium metal composite oxide may be a lithium metal composite oxide made of lithium and any one metal (Me) oxide (MeO x ) selected from the group consisting of Si, Sn, Zn, Mg, Cd, Ce, Ni and Fe, and as an example, may be Li x Fe 2 O 3 (0 ⁇ x ⁇ 1) or LixWO 2 ⁇ 0 ⁇ x ⁇ 1).
  • the conducting material is not particularly limited as long as it has electrical conductivity without causing a chemical change in the relevant battery, and for example, graphite; carbon black such as carbon black, acetylene black, ketjen black, channel black, furnace black, lamp black, and summer black; conductive fibers such as carbon fiber and metal fiber; metal powders such as carbon fluoride, aluminum, and nickel powder; conductive whisker such as zinc oxide and potassium titanate; conductive metal oxide such as titanium oxide; and conductive materials such as polyphenylene derivatives can be used.
  • graphite carbon black such as carbon black, acetylene black, ketjen black, channel black, furnace black, lamp black, and summer black
  • conductive fibers such as carbon fiber and metal fiber
  • metal powders such as carbon fluoride, aluminum, and nickel powder
  • conductive whisker such as zinc oxide and potassium titanate
  • conductive metal oxide such as titanium oxide
  • conductive materials such as polyphenylene derivatives can be used.
  • conductive materials include acetylene black based products of Chevron Chemical Company products or Denka products (Singapore Private Limited), Gulf Oil Company products, Ketjenblack, EC series Armak Company products, Vulcan XC-72 Cabot Company products and Super P (Timcal Company products).
  • the binder is a component that assists in binding of the active material and the conductive material etc. and binding to the current collector, and is usually added in an amount of 1 to 50 wt.% based on the total weight of the mixture containing the electrode active material.
  • An example of such binders includes polyvinylidene fluoride, polyvinyl alcohol, carboxymethyl cellulose (CMC), starch, hydroxypropyl cellulose, regenerated cellulose, polyvinyl pyrrolidone, tetrafluoroethylene, polyethylene, polypropylene, ethylene-propylene-diene terpolymer (EPDM), sulfonated EPDM, styrene butylene rubber, fluorine rubber, various copolymers and the like.
  • the filler is not particularly limited as long as it is a fibrous material without causing chemical change in the relevant battery, and for example, include olefinic polymers such as polyethylene, polypropylene and the like; and fibrous materials such as glass fibers, carbon fibers and the like.
  • a high resistance portion is created at the interface between the electrode active material and the solid a polymer electrolyte material. Accordingly, when the first polymer electrolyte layer and the second polymer electrolyte layer according to the present invention are used to form the all-solid battery, it is possible to reduce the interfacial resistance to the movement of the ions across the interface between the electrode active material and the solid electrolyte material, thereby suppressing the reduction in the output.
  • the first polymer electrolyte layer is disposed facing the negative electrode, the second polymer electrolyte layer is formed thereon, and the positive electrode is formed thereon. If the stacking order of the first and second polymer electrolyte layers is reversed, it is undesirable because the resistance of the battery may increase and thus the discharge capacity may decrease.
  • two polymer electrolyte layers having different EO Li molar ratios of the poly (ethylene oxide)-based polymer and lithium salt, i.e. to simultaneously apply the first polymer electrolyte layer having the molar ratio of EO : Li of the poly (ethylene oxide)-based polymer and the lithium salt of 1 : 1 to 7 : 1 and the second polymer electrolyte layer having the molar ratio of EO : Li of poly (ethylene oxide)-based polymer and lithium salt of 8 : 1 to 30 : 1.
  • the first polymer electrolyte layer is out of the above range, it is undesirable because the interfacial resistance may increase and thus the discharge capacity may decrease, and if the second polymer electrolyte layer is out of the above range, it is undesirable because the resistance of the electrolyte-separation membrane layer may increase and thus the discharge capacity may decrease.
  • the all-solid battery is manufactured through a dry compression process in which electrodes and solid electrolytes are prepared in powder form, then charged into a given mold and then pressed, or a slurry coating process in which a slurry composition including an active material, a solvent, and a binder is prepared, then coated, and then dried.
  • the preparation of the all-solid battery having the above-described composition is not particularly limited in the present invention, and a known method can be used.
  • a cell is assembled by placing the solid electrolyte between the positive electrode and the negative electrode, and then compressing and molding them.
  • the assembled cell is installed in the exterior material and then sealed by heat compression or the like.
  • Laminate packs such as aluminum, stainless steel and the like, or cylindrical or square metal containers are very suitable for the exterior material.
  • the method of coating the electrode slurry on the current collector may include a method of distributing the electrode slurry over the current collector and then uniformly dispersing the slurry using a doctor blade or the like, and methods such as die casting, comma coating, screen printing and the like.
  • the electrode slurry may be bonded to the current collector by pressing or lamination method after forming on a separate substrate. At this time, the thickness of the coating to be finally coated can be adjusted by controlling the concentration of the slurry solution, the number of coatings or the like.
  • the drying process is a process for removing the solvent and moisture in the slurry in order to dry the slurry coated on the metal current collector, and may be changed depending on the solvent used.
  • the drying process is carried out in a vacuum oven at 50 to 200 ⁇ .
  • the drying method may include, for example, a drying method by warm air, hot air, or low-humidity air, vacuum drying, and a drying method by irradiation with (far-) infrared ray or electron beam.
  • the drying time is not particularly limited, but is usually carried out in the range of 30 seconds to 24 hours.
  • a cooling process may be further included, and the cooling process may be a process of slowly cooling to room temperature so that the recrystallized structure of the binder is well formed.
  • a pressing process of passing the electrode between two rolls heated at high temperature and compressing the electrode to a desired thickness can be performed.
  • the pressing process is not particularly limited in the present invention, and a known pressing process is available.
  • the pressing process is carried out by passing between rotating rolls or by using a flat press machine.
  • n in the expression 'PEO n -lithium salt' represents the number of moles of PEO corresponding to 1 mole of Li of the lithium salt and X in the expression 'PEO n -lithium salt-X' means that it is bridged into a semi-IPN structure.
  • a Li symmetric cell was prepared by applying the PEO 5 -LiFSI membrane of Preparation Example 1 to the surface of lithium metal and applying the PEO 20 -LiFSI-X membrane of Preparation Example 3 therebetween.
  • a Li symmetric cell was prepared by applying the PEO 20 -LiFSI-X membrane of Preparation Example 3 between lithium metals.
  • the resistances of the lithium symmetric cells of Example 1 and Comparative Example 1 and the all-solid batteries of Examples 3 and 4 and Comparative Example 4 were measured by electrochemical impedance spectroscopy (EIS), and the interfacial resistances were confirmed by the points where the semicircular lines in the graph of FIG. 1 and FIG. 2 thus obtained meet the x axis.
  • the interfacial resistances are shown in table 2 below. Table 2 Item Symmetric cell All-solid battery Example 1 Comparative Example 1 Example 3 -Example 4 Comparative Example 4 interfacial resistance ( ⁇ ) 130 350 200 350 2200
  • the resistance of the all-solid battery to which PEO 2 -LiFSI and PEO 20 -LiFSI were sequentially applied based on lithium negative electrode which is Example 3
  • the resistance of the all-solid battery to which PEO 20 -LiFSI and PEO 5 -LiFSI were sequentially applied based on lithium negative electrode which is Example 4 in which the positions of the first polymer and the second polymer were changed, was found to be 350 ⁇
  • the resistance of the all-solid battery to which PEO 12 -LiFSI and PEO 20 -LiFSI were sequentially applied based on the lithium negative electrode, which is Comparative Example 4 using only the second polymer was found to be 2200 ⁇ .
  • the interfacial resistance of the battery in which the first polymer electrolyte layer is placed facing the lithium based on the lithium negative electrode and the second polymer electrolyte layer is placed on top of it is lower, and it can be seen that the interfacial resistance of the battery using the first polymer electrolyte layer and the second polymer electrolyte layer at the same time is lower than that of the battery using only the second polymer electrolyte layer.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Condensed Matter Physics & Semiconductors (AREA)
  • Dispersion Chemistry (AREA)
  • Secondary Cells (AREA)
  • Conductive Materials (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Claims (11)

  1. Electrolyte polymère à structure multicouche pour la batterie tout solide, comprenant :
    une première couche d'électrolyte polymère présentant un rapport molaire EO:Li de polymère à base de poly(oxyde d'éthylène) et de sel de lithium compris entre 1:1 et 7:1; et
    une seconde couche d'électrolyte polymère présentant un rapport molaire EO:Li de polymère à base de poly(oxyde d'éthylène) et de sel de lithium compris entre 8:1 et 30:1.
  2. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 1, caractérisé en ce que l'épaisseur de la première couche d'électrolyte polymère est comprise entre 1 et 5 µm.
  3. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 1, caractérisé en ce que l'épaisseur de la seconde couche d'électrolyte polymère est comprise entre 5 et 50 µm.
  4. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 1, caractérisé en ce que le poids moléculaire moyen en poids du polymère à base de poly(oxyde d'éthylène) est compris entre 1000 000 et 8 000 000.
  5. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 1, caractérisé en ce que le sel de lithium comprend un choisi dans le groupe constitué de LiCI, LiBr, LiI, LiClO4, LiBF4, LiB10Cl10, LiPF6, LiCF3SO3, LiCF3CO2, LiAsF6, LiSbF6, LiAlCl4, CH3SO3Li, CF3SO3Li, LiSCN, LiC(CF3SO2)3, (CF3SO2)2NLi, (FSO2)2NLi, lithium de chloroborane, carboxylate aliphatique inférieur de lithium, tétraphénylborate de lithium, imide de lithium et des combinaisons de ceux-ci.
  6. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 1, caractérisé en ce que la seconde couche d'électrolyte polymère est réticulée par un monomère de réticulation pour former des réseaux de polymères semi-interpénétrant.
  7. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 6, caractérisé en ce que le monomère de réticulation comprend des unités répétitives -(CH2-CH2-O)-.
  8. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 7, caractérisé en ce que le monomère de réticulation contient de deux à huit liaisons insaturées alkyléniques aux terminaisons.
  9. Électrolyte polymère à structure multicouche pour la batterie tout solide selon la revendication 6, caractérisé en ce que le monomère de réticulation est contenu en une quantité de 5 à 50 % en poids par rapport au polymère à base de poly(oxyde d'éthylène) et au sel de lithium.
  10. Batterie tout solide comprenant une électrode positive, une électrode négative et un électrolyte polymère solide interposé entre elles, qui est caractérisée en ce que l'électrolyte polymère solide est l'électrolyte polymère selon l'une quelconque des revendications 1 à 9.
  11. Batterie tout solide selon la revendication 10, caractérisée en ce que la première couche d'électrolyte polymère est disposée en regard de l'électrode négative.
EP16860299.3A 2015-10-30 2016-10-28 Électrolyte polymère à structure multicouche, et batterie tout solide le comprenant Active EP3285324B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR20150151630 2015-10-30
PCT/KR2016/012283 WO2017074116A1 (fr) 2015-10-30 2016-10-28 Électrolyte polymère à structure multicouche, et batterie tout solide le comprenant

Publications (3)

Publication Number Publication Date
EP3285324A1 EP3285324A1 (fr) 2018-02-21
EP3285324A4 EP3285324A4 (fr) 2018-12-19
EP3285324B1 true EP3285324B1 (fr) 2020-01-01

Family

ID=58742443

Family Applications (1)

Application Number Title Priority Date Filing Date
EP16860299.3A Active EP3285324B1 (fr) 2015-10-30 2016-10-28 Électrolyte polymère à structure multicouche, et batterie tout solide le comprenant

Country Status (5)

Country Link
US (1) US10522872B2 (fr)
EP (1) EP3285324B1 (fr)
JP (1) JP6450030B2 (fr)
KR (1) KR101930477B1 (fr)
CN (1) CN107636880B (fr)

Families Citing this family (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102093970B1 (ko) * 2017-06-20 2020-04-23 주식회사 엘지화학 다층 구조 고분자 고체 전해질 및 이를 포함하는 전고체 전지
DE102017211413A1 (de) * 2017-07-05 2019-01-10 Robert Bosch Gmbh Negative Elektrode mit Elektroden-, Zwischen- und Festelektrolytschicht
KR102536633B1 (ko) * 2018-03-14 2023-05-25 주식회사 엘지에너지솔루션 양극의 제조 방법
KR102346844B1 (ko) * 2018-07-25 2022-01-03 주식회사 엘지에너지솔루션 고분자 전해질 및 이의 제조방법
CN110828883B (zh) * 2018-08-08 2021-09-03 比亚迪股份有限公司 一种锂离子电池及其制备方法和电动车辆
KR102517991B1 (ko) 2018-09-28 2023-04-03 주식회사 엘지에너지솔루션 고분자계 고체 전해질을 포함하는 전극의 제조 방법 및 그 방법으로 제조된 전극
KR102395655B1 (ko) * 2018-10-11 2022-05-06 주식회사 엘지에너지솔루션 복합 전해질막 및 상기 복합 전해질막을 포함하는 전고체 전지
CN111566866B (zh) * 2018-10-31 2024-01-05 株式会社Lg新能源 具有差异离子电导率的电解质和包含该电解质的锂二次电池
EP3754760A4 (fr) * 2018-10-31 2021-05-26 Lg Chem, Ltd. Accumulateur au lithium
CN111435761B (zh) * 2019-01-11 2021-08-10 荣盛盟固利新能源科技有限公司 一种全固态锂离子电池及其多层电解质膜热压制备的方法
JP7245100B2 (ja) * 2019-04-02 2023-03-23 積水化学工業株式会社 リチウムイオン二次電池
KR102435217B1 (ko) * 2019-04-09 2022-08-24 광주과학기술원 그래프팅된 고분자 및 이를 포함하는 이차전지용 고체 전해질 조성물
US11309585B2 (en) 2019-04-19 2022-04-19 International Business Machines Corporation Molten ion conductive salt/silicon interface for decreased interfacial resistance
US11205800B2 (en) 2019-04-19 2021-12-21 International Business Machines Corporation Polymer and molten ion conductive salt and silicon interface for decreased interfacial resistance
DE102019127616A1 (de) * 2019-10-14 2021-04-15 Forschungszentrum Jülich GmbH Semi-interpenetrierende Polymernetzwerke als Separatoren für den Einsatz in Alkali-Metall-Batterien
JP6803451B1 (ja) 2019-12-13 2020-12-23 住友化学株式会社 リチウム金属複合酸化物、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
JP6804625B1 (ja) 2019-12-17 2020-12-23 住友化学株式会社 リチウム金属複合酸化物粉末、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
JP6857752B1 (ja) 2020-01-09 2021-04-14 住友化学株式会社 リチウム金属複合酸化物、リチウム二次電池用正極活物質、リチウム二次電池用正極、リチウム二次電池及びリチウム金属複合酸化物の製造方法
JP6935526B2 (ja) 2020-02-26 2021-09-15 住友化学株式会社 リチウム金属複合酸化物、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
WO2021192278A1 (fr) * 2020-03-27 2021-09-30 TeraWatt Technology株式会社 Batterie solide
JP6861870B1 (ja) 2020-04-14 2021-04-21 住友化学株式会社 リチウム二次電池用正極活物質粒子、リチウム二次電池用正極及びリチウム二次電池
JP7471903B2 (ja) 2020-05-07 2024-04-22 住友化学株式会社 リチウム金属複合酸化物、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
JP6980053B2 (ja) 2020-05-07 2021-12-15 住友化学株式会社 リチウム二次電池用正極活物質前駆体、リチウム二次電池用正極活物質前駆体の製造方法及びリチウム二次電池用正極活物質の製造方法
JP6964724B1 (ja) 2020-06-29 2021-11-10 住友化学株式会社 リチウム二次電池正極活物質用前駆体及びリチウム二次電池正極活物質の製造方法
JP7233402B2 (ja) 2020-07-06 2023-03-06 住友化学株式会社 リチウム二次電池正極活物質用前駆体、リチウム金属複合酸化物、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
CN112038692B (zh) * 2020-08-10 2022-04-26 江苏正力新能电池技术有限公司 固态电解质膜、固态锂离子电池及其制备方法
CA3189305A1 (fr) 2020-08-19 2022-02-24 Yuki Matsumoto Procede de production d'un oxyde composite metallique de lithium
JPWO2022044720A1 (fr) 2020-08-24 2022-03-03
JP6976392B1 (ja) 2020-09-04 2021-12-08 住友化学株式会社 リチウム金属複合酸化物、リチウム二次電池用正極及びリチウム二次電池
JP6923730B1 (ja) 2020-09-04 2021-08-25 住友化学株式会社 リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
CN116438683A (zh) 2020-11-17 2023-07-14 住友化学株式会社 锂金属复合氧化物的制造方法
JP6930015B1 (ja) 2020-11-19 2021-09-01 住友化学株式会社 前駆体、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
CA3199449A1 (fr) 2020-11-24 2022-06-02 Yuki Matsumoto Procede de production d'un oxyde composite de lithium et de metal
JP7031100B1 (ja) 2020-12-14 2022-03-08 株式会社Abri リチウム二次電池用ゲル電解質、リチウム二次電池およびリチウム二次電池の製造方法
CN112687960A (zh) * 2020-12-28 2021-04-20 浙江省科创新材料研究院 一种利用锌盐稳定固态电解质/金属负极界面的方法
JP7118187B1 (ja) 2021-02-03 2022-08-15 住友化学株式会社 リチウム金属複合酸化物、リチウム二次電池用正極活物質、リチウム二次電池用正極及びリチウム二次電池
JP7116267B1 (ja) 2021-03-16 2022-08-09 住友化学株式会社 金属複合化合物、リチウム金属複合酸化物の製造方法及び金属複合化合物の製造方法
WO2022209506A1 (fr) 2021-03-31 2022-10-06 住友化学株式会社 Matériau actif d'électrode négative pour batterie rechargeable au lithium, électrode négative métallique et batterie rechargeable au lithium
CN115275362B (zh) * 2022-07-29 2023-06-23 中国地质大学(武汉) 含有异质离子凝胶缓冲层的固态电解质及其制备和应用

Family Cites Families (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05298915A (ja) 1992-04-16 1993-11-12 Japan Energy Corp 電解質複合体
JP3677782B2 (ja) * 1992-10-24 2005-08-03 ソニー株式会社 高分子固体電解質
KR0125151B1 (ko) 1994-12-30 1997-12-15 이정성 복합 고분자 전해질을 갖는 전지(電池)
JPH08329983A (ja) * 1995-06-06 1996-12-13 Matsushita Electric Ind Co Ltd リチウム電池
EP1057869B1 (fr) * 1998-12-17 2004-06-02 Nisshinbo Industries, Inc. Composition pour polyelectrolyte conducteur par migration des ions et polyelectrolyte solide conducteur par migration des ions
JP2000285929A (ja) 1999-03-31 2000-10-13 Sony Corp 固体電解質電池
JP3640863B2 (ja) 2000-05-25 2005-04-20 トヨタ自動車株式会社 イオン伝導性固体電解質
KR100406690B1 (ko) 2001-03-05 2003-11-21 주식회사 엘지화학 다성분계 복합 필름을 이용한 전기화학소자
JP2003303621A (ja) * 2002-04-09 2003-10-24 Toyota Motor Corp ポリマー電解質およびポリマーリチウム電池
JP2004206942A (ja) 2002-12-24 2004-07-22 Ion Engineering Research Institute Corp 全固体リチウム電池
JP4560721B2 (ja) 2004-11-18 2010-10-13 ダイソー株式会社 電解質組成物および電池
FR2881275B1 (fr) 2005-01-24 2007-04-27 Batscap Sa Electrolyte bicouche pour batterie au lthium
JP2008226637A (ja) * 2007-03-13 2008-09-25 Matsushita Electric Ind Co Ltd 全固体型ポリマー電池およびその製造方法
WO2008118749A2 (fr) 2007-03-23 2008-10-02 Novozymes Biologicals, Inc. Prévention et réduction de la formation de biofilms et de la prolifération du plancton
US20090162754A1 (en) * 2007-12-21 2009-06-25 Bathium Canada Inc. Electrolyte for lithium polymer batteries
US9178255B2 (en) 2008-06-20 2015-11-03 University Of Dayton Lithium-air cells incorporating solid electrolytes having enhanced ionic transport and catalytic activity
ITRM20090161A1 (it) 2009-04-08 2010-10-09 Jusef Hassoun Accumulatori litio-zolfo
JP5548937B2 (ja) 2009-08-25 2014-07-16 国立大学法人三重大学 イオン伝導性高分子固体電解質
KR101313156B1 (ko) * 2009-12-04 2013-09-30 주식회사 아모그린텍 다성분계 나노 복합산화물 분말과 그 제조방법, 이를 이용한 전극의 제조방법과 이를 이용한 박막 전지 및 그 제조방법
KR101439716B1 (ko) 2010-02-10 2014-09-12 고쿠리츠다이가쿠호진 미에다이가쿠 고체 전해질용 조성물, 고체 전해질, 리튬 이온 2차 전지 및 리튬 이온 2차 전지의 제조방법
JP5382536B2 (ja) 2010-02-25 2014-01-08 ダイソー株式会社 高分子固体電解質およびその用途
KR20120092918A (ko) 2011-02-14 2012-08-22 한양대학교 산학협력단 리튬 이차 전지용 고분자 복합 전해질 및 이를 포함하는 리튬 이차 전지
JP5664865B2 (ja) 2011-03-07 2015-02-04 日産化学工業株式会社 ゲル電解質
KR101422908B1 (ko) * 2012-04-02 2014-07-23 삼성정밀화학 주식회사 리튬이온 이차전지용 전해질 및 이것을 포함하는 리튬이온 이차전지
JP6017872B2 (ja) 2012-07-26 2016-11-02 小島プレス工業株式会社 リチウムイオン二次電池及びその製造方法並びに製造装置
JP5885624B2 (ja) 2012-08-31 2016-03-15 積水化学工業株式会社 リチウムイオン二次電池
KR101625707B1 (ko) 2012-12-21 2016-06-14 주식회사 엘지화학 전기화학소자용 고체 전해질 및 이를 구비한 전기화학소자
WO2014133024A1 (fr) 2013-02-27 2014-09-04 ダイソー株式会社 Électrode positive et batterie secondaire à électrolyte non-aqueux
KR101375214B1 (ko) 2013-03-08 2014-03-17 주식회사 아모그린텍 다성분계 나노 복합산화물 분말을 이용한 박막 전지 및 그 제조방법
KR101613511B1 (ko) 2014-02-26 2016-04-19 서강대학교산학협력단 고체 고분자 전해질 조성물 및 이를 포함하는 리튬 이차전지

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
EP3285324A1 (fr) 2018-02-21
EP3285324A4 (fr) 2018-12-19
US20180159169A1 (en) 2018-06-07
US10522872B2 (en) 2019-12-31
JP2018514929A (ja) 2018-06-07
CN107636880B (zh) 2020-07-10
JP6450030B2 (ja) 2019-01-09
KR20170051324A (ko) 2017-05-11
KR101930477B1 (ko) 2018-12-18
CN107636880A (zh) 2018-01-26

Similar Documents

Publication Publication Date Title
EP3285324B1 (fr) Électrolyte polymère à structure multicouche, et batterie tout solide le comprenant
EP2036149B1 (fr) Matériau actif de cathode et batterie secondaire au lithium le contenant
EP3467907B1 (fr) Procédé de fabrication d'une électrode comprenant un électrolyte polymère et électrode ainsi fabriquée
KR102093972B1 (ko) 리튬 이차전지
EP3633768A2 (fr) Batterie secondaire au lithium
KR102024889B1 (ko) 반 상호침투 고분자 네트워크 구조의 고분자 전해질 및 이를 포함하는 전고체 전지
US20160164138A1 (en) Organic/inorganic composite electrolyte, electrode-electrolyte assembly and lithium secondary battery including the same, and manufacturing method of the electrode-electrolyte assembly
US11764358B2 (en) Method for manufacturing all solid-state battery comprising polymeric solid electrolyte and all solid-state battery obtained thereby
KR102328261B1 (ko) 리튬 이차전지
US9269951B2 (en) Cathode active material and lithium secondary battery containing them
KR102564970B1 (ko) 음극 및 이를 포함하는 이차전지
US20210020917A1 (en) Method for Manufacturing Electrode Comprising Polymeric Solid Electrolyte and Electrode Obtained Thereby
KR102006717B1 (ko) 질산리튬을 포함하는 고분자 전해질 및 이를 포함하는 전고체 전지
KR20190060719A (ko) 이중층 구조의 활물질층을 포함하는 음극, 이의 제조방법 및 이를 포함하는 이차전지
KR20190107648A (ko) 전극조립체를 구성하는 분리막의 기공 내에 겔화 전해액 성분을 포함하고 있는 전지셀
KR20190127603A (ko) 고분자계 고체 전해질을 포함하는 전극의 제조 방법 및 그 방법으로 제조된 전극
KR102098154B1 (ko) 3차원 망상 구조의 전극 집전체를 포함하는 전극
KR20170041470A (ko) 전극조립체를 구성하는 분리막의 기공 내에 겔화 전해액 성분을 포함하고 있는 전지셀
KR20210120686A (ko) 음극의 제조방법
KR20200135060A (ko) 리튬 이차전지용 양극, 이의 제조방법 및 이를 포함한 리튬 이차전지
KR102567400B1 (ko) 이차전지
CN114784372A (zh) 一种复合固态电解质的制备方法
US20220285744A1 (en) Battery system, and method of using the same and battery pack including the same
KR102130051B1 (ko) 이차전지용 전극의 제조방법, 상기 제조방법으로 제조된 이차전지용 전극 및 상기 이차전지용 전극을 포함하는 이차전지
KR20130118243A (ko) 이차전지용 전극

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20171115

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

A4 Supplementary search report drawn up and despatched

Effective date: 20181119

RIC1 Information provided on ipc code assigned before grant

Ipc: H01M 10/0585 20100101ALI20181113BHEP

Ipc: H01M 10/0565 20100101AFI20181113BHEP

Ipc: H01M 10/0568 20100101ALI20181113BHEP

Ipc: H01M 10/056 20100101ALI20181113BHEP

Ipc: H01M 10/052 20100101ALI20181113BHEP

Ipc: H01M 2/16 20060101ALI20181113BHEP

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20190823

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

Ref country code: AT

Ref legal event code: REF

Ref document number: 1220940

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200115

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602016027588

Country of ref document: DE

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20200101

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200527

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200401

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200402

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200501

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200401

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602016027588

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 1220940

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200101

26N No opposition filed

Effective date: 20201002

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20201028

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20201031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20201031

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20201031

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20201031

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20201028

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20200101

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230408

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 602016027588

Country of ref document: DE

Owner name: LG ENERGY SOLUTION, LTD., KR

Free format text: FORMER OWNER: LG CHEM. LTD., SEOUL, KR

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

Free format text: REGISTERED BETWEEN 20230824 AND 20230831

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20230920

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20230922

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20230920

Year of fee payment: 8